JP2000290013A - Production of alumina particle - Google Patents

Production of alumina particle

Info

Publication number
JP2000290013A
JP2000290013A JP11100077A JP10007799A JP2000290013A JP 2000290013 A JP2000290013 A JP 2000290013A JP 11100077 A JP11100077 A JP 11100077A JP 10007799 A JP10007799 A JP 10007799A JP 2000290013 A JP2000290013 A JP 2000290013A
Authority
JP
Japan
Prior art keywords
alumina
aluminate
alumina particles
aluminum salt
mixture
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP11100077A
Other languages
Japanese (ja)
Other versions
JP3711318B2 (en
Inventor
Takeshi Morimura
剛 森村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
YKK Corp
Original Assignee
YKK Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by YKK Corp filed Critical YKK Corp
Priority to JP10007799A priority Critical patent/JP3711318B2/en
Publication of JP2000290013A publication Critical patent/JP2000290013A/en
Application granted granted Critical
Publication of JP3711318B2 publication Critical patent/JP3711318B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Cosmetics (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain a particle having large aspect ratio, narrow particle size distribution and smooth particle surface by firing a mixture containing alumina or alumina hydrate and a neutralized metallic salt, which are obtained by reacting an aluminate with an acidic aluminum salt in the presence of water, at a specific temp. SOLUTION: The mixture containing the alumina or the alumina hydrate and the neutralized metallic salt are produced by reacting the aluminate with the acidic aluminum salt in a state containing water. The mixture is fired at 1,000-1,600 deg.C to produce the alumina particle. The alumina or the alumina hydrate is amorphous. Alternatively, the alumina or the alumina hydrate obtained by reacting one prepared by adding an alkaline phosphate into the aluminate with the acidic aluminum salt in the state containing water is used. As a result, the plate like alumina particle having about 0.2-100 μm average particle diameter, about <=3 μm thickness and the aspect ratio of about >=5 is obtained.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明はアルミナ粒子特には
板状アルミナ粒子の製造方法に関するものであり、板状
アルミナ粒子にあってはさらに詳しくはアスペクト比が
大きく、粒度分布の狭い粒子表面が滑らかな板状アルミ
ナ粒子を提供し、研磨剤、充填材、化粧料、セラミック
原料、顔料、さらには表面に金属酸化物をコーティング
することにより光輝性顔料としても有用な材料を提供す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing alumina particles, particularly plate-like alumina particles, and more particularly, to a plate-like alumina particle having a large aspect ratio and a narrow particle size distribution. The present invention provides a plate-like alumina particle, and provides an abrasive, a filler, a cosmetic, a ceramic raw material, a pigment, and a material useful as a glitter pigment by coating the surface with a metal oxide.

【0002】[0002]

【従来の技術】従来、アルミナ粒子特には板状の形態を
有するアルミナ粒子の製造方法としては、特許2654
276号公報にみられるような水熱処理による方法(以
下水熱合成法)や特開平9−227337号公報にみら
れるようなフッ素系の鉱化剤の存在下で焼成する方法等
が知られている。
2. Description of the Related Art Conventionally, a method for producing alumina particles, particularly, alumina particles having a plate-like form is disclosed in Japanese Patent No. 2654.
A method by hydrothermal treatment (hereinafter referred to as a hydrothermal synthesis method) as disclosed in Japanese Patent Application Laid-Open No. 276/276 and a method of firing in the presence of a fluorine-based mineralizer as disclosed in Japanese Patent Application Laid-Open No. 9-227337 are known. I have.

【0003】しかし、水熱合成法は、製造方法の観点か
らみて高温反応処理装置を必要とし、設備投資が大掛か
りなものとなり不利であるとともに、製法としても高温
・高圧下での合成であるため、得られる粉体は高価にな
るという問題があった。また、水酸化アルミニウムをハ
ロゲン系のガスの存在下で焼成する方法は、焼成時に発
生するハロゲンガスの処理問題が存在する。さらには酸
性アルミニウム塩に炭酸アルカリ塩を用いて焼成する方
法もあるが、この方法だと中和する時に大量の炭酸が発
生し、扱いにくい問題がある。
However, the hydrothermal synthesis method requires a high-temperature reaction apparatus from the viewpoint of the production method, is disadvantageous in that the capital investment becomes large, and the production method is a synthesis under high temperature and high pressure. However, there is a problem that the obtained powder becomes expensive. Further, the method of firing aluminum hydroxide in the presence of a halogen-based gas has a problem of treating halogen gas generated during firing. Further, there is a method of calcining using an acidic aluminum salt with an alkali carbonate, but this method has a problem that a large amount of carbonic acid is generated at the time of neutralization and is difficult to handle.

【0004】[0004]

【発明が解決しようとする課題】本発明は、このような
従来技術における多くの課題を改善することを目的と
し、凝集のない粒度分布がシャープなアルミナ粒子さら
にはこれらを含み表面が滑らかな板状アルミナ粒子の簡
便な製造方法を提供することを目的とする。
SUMMARY OF THE INVENTION It is an object of the present invention to solve many of the problems in the prior art, and it is an object of the present invention to provide an alumina particle having a sharp particle size distribution without agglomeration, and a plate containing these particles having a smooth surface. It is an object of the present invention to provide a simple method for producing alumina particles.

【0005】[0005]

【課題を解決するための手段】本発明は、下記の構成よ
りなる。
The present invention comprises the following constitutions.

【0006】(1)アルミン酸塩と酸性アルミニウム塩
とを水を含んだ状態で反応させることにより、アルミナ
又は/及びアルミナ水和物と中和金属塩を含む混合物を
製造し、この混合物を1000〜1600℃で焼成する
ことを特徴とするアルミナ粒子の製造方法。
(1) A mixture containing alumina or / and alumina hydrate and a neutralized metal salt is produced by reacting an aluminate and an acidic aluminum salt in a state containing water, and this mixture is mixed with 1000 parts. A method for producing alumina particles, characterized by firing at 1600 ° C.

【0007】(2)アルミナ又は/及びアルミナ水和物
が非晶質又は/及び結晶質である上記(1)記載のアル
ミナ粒子の製造方法。 (3)アルミン酸塩と酸性アルミニウム塩と燐酸塩とを
水を含んだ状態で反応させる(1)記載のアルミナ粒子
の製造方法。
(2) The method for producing alumina particles according to the above (1), wherein the alumina or / and alumina hydrate is amorphous or / and crystalline. (3) The method for producing alumina particles according to (1), wherein the aluminate, the acidic aluminum salt and the phosphate are reacted in a state containing water.

【0008】(4)アルミン酸塩にアルカリ性の燐酸塩
を添加したものと酸性アルミニウム塩を混合したものを
水分を含んだ状態で反応させる上記(1)記載のアルミ
ナ粒子の製造方法。 (5)アルミン酸塩と酸性アルミニウム塩に酸性の燐酸
塩を添加したものを水分を含んだ状態で反応させる上記
(1)記載のアルミナ粒子の製造方法。 (6)アルミン酸塩と酸性アルミニウム塩と燐酸塩とを
混合した時の水素イオン濃度がpH=6〜10の範囲で
ある上記(3)〜(5)のいずれかに記載のアルミナ粒
子の製造方法。
(4) The method for producing alumina particles according to the above (1), wherein a mixture of an aluminate to which an alkaline phosphate is added and a mixture of an acidic aluminum salt are reacted while containing water. (5) The method for producing alumina particles according to the above (1), wherein an aluminate and an acidic aluminum salt to which an acidic phosphate is added are reacted in a state containing water. (6) The production of alumina particles according to any of (3) to (5) above, wherein the hydrogen ion concentration when the aluminate, the acidic aluminum salt and the phosphate are mixed is in the range of pH = 6 to 10. Method.

【0009】(7)平均粒子径が0.2〜100μm、
厚みが3μm以下、アスペクト比(粒子径/厚み)が5
以上である板状アルミナ粒子を製造する上記(3)〜
(6)のいずれかに記載のアルミナ粒子の製造方法。
(7) an average particle diameter of 0.2 to 100 μm;
Thickness of 3 μm or less, aspect ratio (particle diameter / thickness) of 5
The above (3) to above for producing plate-like alumina particles as described above
The method for producing alumina particles according to any one of (6).

【0010】本発明において用いられるアルミン酸塩は
水酸化アルカリの溶液にアルミニウム又は水酸化アルミ
ニウムを溶かしたものであれば何でもよく、例えばNa
AlO2、KAlO2のようなMAlO2(Mは一価の金
属)の構造式をとるアルカリ金属塩やNaAlO2・5
/4H2O、NaAlO2・3H2O、KAlO2・3/2
2OのようなMAlO2・nH2O(Mは一価の金属)
の構造式をとるもの、更には一般式でxM2O・yAl2
3・zH2O(Mは一価の金属、z=0を含む)の構造
式をとるものである。又、酸性アルミニウム塩は、酸性
溶液にアルミニウム又は水酸化アルミニウムを溶かした
ものであれば何でもよく、酸性溶液としては例えば燐酸
や硫酸のような鉱酸または蓚酸やマレイン酸、マロン酸
のような有機酸が挙げられる。具体的には硫酸アルミニ
ウム、塩化アルミニウムなどがある。
The aluminate used in the present invention may be any one obtained by dissolving aluminum or aluminum hydroxide in an alkali hydroxide solution.
An alkali metal salt having a structural formula of MAlO 2 (M is a monovalent metal) such as AlO 2 or KAlO 2 or NaAlO 2 .5
/ 4H 2 O, NaAlO 2 · 3H 2 O, KAlO 2 · 3/2
MAlO 2 .nH 2 O such as H 2 O (M is a monovalent metal)
And the general formula xM 2 O.yAl 2
It has a structural formula of O 3 .zH 2 O (M is a monovalent metal, including z = 0). The acidic aluminum salt may be any solution in which aluminum or aluminum hydroxide is dissolved in an acidic solution. Examples of the acidic solution include mineral acids such as phosphoric acid and sulfuric acid and organic acids such as oxalic acid, maleic acid and malonic acid. Acids. Specific examples include aluminum sulfate and aluminum chloride.

【0011】又、燐酸塩は結晶成長剤としての作用があ
り、板状アルミナを作製する上では必要であり、燐酸、
燐酸ソーダ、燐酸カリ、燐酸アンモニウム、ピロ燐酸ソ
ーダ、ピロ燐酸カリ、トリポリ燐酸ソーダ、トリポリ燐
酸アンモニウムなどが挙げることができる。この燐酸塩
の添加量は、アルミナに換算して0.01重量%以上で
あることが好ましい。アルミン酸塩に酸性アルミニウム
塩又はこれに燐酸塩を混合した水溶液を混合し、加水分
解生成物と中和塩を含む懸濁液またはゲルとする。中和
塩は焼成時において、溶融状態となり、このときアルミ
ナ化及びアルミナの板状化を促進する効果があり、中和
の量はアルミナ重量1に対して0.1〜7倍が好まし
い。0.1倍未満ではアルミナ化及びアルミナの板状化
に十分な効果を発揮せず、また7倍を超えると洗浄時に
相当な負担がかかるためである。
Phosphate acts as a crystal growth agent and is necessary for producing plate-like alumina.
Examples include sodium phosphate, potassium phosphate, ammonium phosphate, sodium pyrophosphate, potassium pyrophosphate, sodium tripolyphosphate, and ammonium tripolyphosphate. The amount of the phosphate is preferably 0.01% by weight or more in terms of alumina. The aluminum salt is mixed with an acidic aluminum salt or an aqueous solution obtained by mixing a phosphate with the aluminum salt to form a suspension or gel containing a hydrolysis product and a neutralization salt. The neutralized salt is in a molten state at the time of firing, and has an effect of promoting aluminization and plate formation of alumina. The amount of neutralization is preferably 0.1 to 7 times the weight of alumina. If the ratio is less than 0.1 times, sufficient effect for alumina conversion and plate formation of alumina is not exerted, and if the ratio exceeds 7 times, a considerable load is imposed upon cleaning.

【0012】その後乾燥粉末を1000〜1600℃で
焼成する焼成温度が1000℃未満であるとアルミナ化
(特には板状アルミナ化)するまでに長時間を要し、経
済的ではなく、又、1600℃を越えるとアルミナ(特
には板状アルミナ)の粒子同士が焼結をしてしまうため
である。このような焼結をより確実に防ぐためには、焼
成温度を1400℃以下とすることがより好ましい。
If the firing temperature at which the dried powder is fired at 1000 to 1600 ° C. is lower than 1000 ° C., it takes a long time to aluminize (particularly plate-like alumina), which is not economical. If the temperature exceeds ℃, alumina (particularly, plate-like alumina) particles are sintered. In order to more reliably prevent such sintering, the firing temperature is more preferably set to 1400 ° C. or lower.

【0013】水素イオン濃度をpH6〜10の範囲にし
た場合、アルミナ水和物の析出が効率的になされ、アル
ミナ(特には板状アルミナ)を効率良く製造することが
できる。非晶質アルミナ又は/及び結晶質アルミナ粒子
と中和金属塩との混合物は、焼成後に生成される粒子同
士の凝集を防ぐため、焼成前に蒸散乾燥し、その後、混
合物を解することが好ましい。又、焼成後においては、
熔融塩処理し固形分を得た後、この固形分を水洗し、濾
取し乾燥することが好ましい。
When the hydrogen ion concentration is in the range of pH 6 to 10, alumina hydrate is efficiently precipitated, and alumina (particularly, plate-like alumina) can be efficiently produced. The mixture of the amorphous alumina and / or crystalline alumina particles and the neutralized metal salt is preferably evaporated and dried before firing, and then the mixture is disintegrated, in order to prevent aggregation of the particles generated after firing. . Also, after firing,
After obtaining a solid content by performing a molten salt treatment, it is preferable that the solid content be washed with water, collected by filtration, and dried.

【0014】このようにして得られた本発明に係るアル
ミナ粒子の場合、平均粒子径の0.2〜100μmの粒
状アルミナ粒子であり、特に板状アルミナ粒子はSEM
観察の結果、大きな平均粒子径で0.2〜100μm、
厚みが3μm以下アスペクト比(粒子径/厚み)が5以
上である板状アルミナ粒子であり、水に対して分散し撹
拌したところ、流線(偏平粒子を液中に懸濁させ撹拌さ
せた際に分散性が良いと粒子の一連の流れが粒子表面の
反射光が層状の縞模様となって観察される現象)がみら
れ、分散性が極めて良好なものであった。板状アルミナ
粒子を分析した結果、リン及びリン化合物や中和塩が検
出されず、洗浄工程において除去されているものと考え
られる。
The alumina particles according to the present invention thus obtained are granular alumina particles having an average particle diameter of 0.2 to 100 μm, and particularly, plate-like alumina particles are SEM.
As a result of the observation, a large average particle diameter of 0.2 to 100 μm,
A plate-like alumina particle having a thickness of 3 μm or less and an aspect ratio (particle diameter / thickness) of 5 or more. When dispersed and stirred in water, streamline (when flat particles are suspended in a liquid and stirred) When the dispersibility is good, a phenomenon in which a series of flow of particles is observed as reflected light on the particle surface as a layered stripe pattern) was observed, and the dispersibility was extremely good. As a result of analyzing the plate-like alumina particles, it is considered that phosphorus, the phosphorus compound, and the neutralized salt were not detected, and were removed in the washing step.

【0015】本発明に係るアルミナ粒子及び板状アルミ
ナ粒子はそのままセラミックスの原料とすることがで
き、あるいは塗料用、プラスチック等の充填剤、化粧料
用、研磨剤、釉薬用等の顔料として優れているものであ
る。特に板状アルミナ粒子の場合、前述の用途に有用で
あり、さらに金属酸化物をコーティングすることによっ
て光輝性顔料としての有用性はさらに増す。
The alumina particles and plate-like alumina particles according to the present invention can be used as raw materials for ceramics as they are, or they are excellent as pigments for paints, fillers such as plastics, cosmetics, abrasives, glazes and the like. Is what it is. In particular, in the case of plate-like alumina particles, they are useful for the above-mentioned applications. Further, by coating a metal oxide, the usefulness as a glitter pigment is further increased.

【0016】[0016]

【発明の実施の形態】次に実施例により本発明を更に詳
細に説明するが、本発明はこれらの実施例に限定される
ものではない。
Next, the present invention will be described in more detail with reference to examples, but the present invention is not limited to these examples.

【0017】実施例1 水酸化ナトリウム20gを水中で溶液とし、この溶液に
金属アルミニウム5g及び燐酸水素2ナトリウム0.2
5g入れ溶液中に撹拌しながら溶かす。その後この混合
溶液中に硫酸アルミニウム水溶液をpH=7になるまで
撹拌しながら投入する。混合したものは白濁状のゲルと
なり、これをそのまま蒸散乾燥した。この時の蒸散乾燥
した固形分のX線回折の結果、結晶質のものとして硫酸
ナトリウムが同定された。その後1200℃で5時間保
持の条件で焼成した。得られた処理物に水を加え洗浄、
濾過し、固形分を乾燥し板状アルミナ粉体を得た。得ら
れた板状アルミナをX線回折法により生成物を同定した
ところ、酸化アルミニウム(αアルミナ)であった。S
EMにて観察してみたところ板状粒子であり、粒度分布
計で粒度を測定したところ中心粒径が10μmであり、
シャープな分布となっていた。又、この粉末を水に混ぜ
てみたところ、きれいな流紋が確認された。 実施例2 水酸化ナトリウム20gを60℃の水中で溶液とし、こ
の溶液に金属アルミニウム5g及び燐酸水素2ナトリウ
ム0.25g入れ溶液中に撹拌しながら溶かす。その後
この混合溶液中に60℃の硫酸アルミニウム水溶液をp
H=9になるまで撹拌しながら投入する。混合したもの
は白濁状のゲルとなり、そのまま更に60分撹拌した
後、蒸散乾燥した。この時の蒸散乾燥した固形分のX線
回折の結果、擬ベーマイトである事を確認した。蒸散乾
燥した固形分を1200℃で5時間保持の条件で焼成し
た。得られた処理物に水を加え洗浄、濾過し、固形分を
乾燥し板状アルミナ粉体を得た。得られた板状アルミナ
をX線回折法により生成物を同定したところ、酸化アル
ミニウム(αアルミナ)であった。SEMにて観察して
みたところ板状粒子であり、粒度分布計で粒度を測定し
たところ中心粒径が10μmであり、シャープな分布と
なっていた。又、この粉末を水に混ぜてみたところ、き
れいな流紋が確認された。
Example 1 A solution of 20 g of sodium hydroxide in water was added to 5 g of metallic aluminum and 0.2 g of disodium hydrogen phosphate.
Add 5 g and dissolve into the solution with stirring. Thereafter, an aqueous solution of aluminum sulfate is introduced into the mixed solution with stirring until the pH becomes 7. The resulting mixture turned into a cloudy gel, which was evaporated and dried as it was. As a result of X-ray diffraction of the evaporated and dried solid, sodium sulfate was identified as a crystalline substance. Then, it was baked at 1200 ° C. for 5 hours. Water is added to the obtained processed material and washed,
After filtration, the solid content was dried to obtain a plate-like alumina powder. When the product of the obtained plate-like alumina was identified by an X-ray diffraction method, it was found to be aluminum oxide (α-alumina). S
When observed with EM, it was plate-like particles, and the particle size was measured with a particle size distribution analyzer, and the central particle size was 10 μm.
It had a sharp distribution. Further, when this powder was mixed with water, a clean ripple was confirmed. Example 2 20 g of sodium hydroxide was made into a solution in water at 60 ° C., and 5 g of metallic aluminum and 0.25 g of disodium hydrogen phosphate were put into this solution and dissolved in the solution with stirring. Thereafter, an aqueous solution of aluminum sulfate at 60 ° C.
Charge with stirring until H = 9. The resulting mixture became a cloudy gel, and the mixture was further stirred for 60 minutes and then evaporated to dryness. As a result of X-ray diffraction of the evaporated and dried solid, it was confirmed to be pseudo-boehmite. The evaporated and dried solid was fired at 1200 ° C. for 5 hours. Water was added to the obtained treated product, which was washed, filtered, and the solid content was dried to obtain a plate-like alumina powder. When the product of the obtained plate-like alumina was identified by an X-ray diffraction method, it was found to be aluminum oxide (α-alumina). Observation with an SEM revealed that the particles were plate-like particles, and the particle size was measured with a particle size distribution meter. The central particle size was 10 μm, and the distribution was sharp. Further, when this powder was mixed with water, a clean ripple was confirmed.

【0018】実施例3 アルミン酸ナトリウム20gを60℃の水に溶解させ、
その中に硫酸アルミニウム水溶液を加えpH=9になる
ように調整し、そのまま60分撹拌した。その後蒸散乾
燥させ、乾燥した固形分のX線回折の結果、擬ベーマイ
トの回折ピークが確認された。この乾燥固形分を120
0℃、5時間焼成し、洗浄、濾過し、固形分を乾燥し
た。得られた物をX線回折により同定した結果、酸化ア
ルミナ(αアルミナ)であった。SEMにて観察してみ
たところ、0.2μmの粒状であり、板状粒子ではなか
った。又、この粉末を水に混ぜてみたところ、流紋が確
認されなかった。
Example 3 20 g of sodium aluminate was dissolved in water at 60 ° C.
An aqueous solution of aluminum sulfate was added thereto to adjust the pH to 9, and the mixture was stirred for 60 minutes. Thereafter, it was evaporated and dried, and as a result of X-ray diffraction of the dried solid, a diffraction peak of pseudo-boehmite was confirmed. This dry solid content is 120
The mixture was baked at 0 ° C. for 5 hours, washed, filtered, and the solid content was dried. As a result of identifying the obtained product by X-ray diffraction, it was found to be alumina oxide (α-alumina). Observation with an SEM revealed that the particles were 0.2 μm in particle size and not plate-like particles. Further, when this powder was mixed with water, no ripple was observed.

【0019】[0019]

【発明の効果】本発明によれば凝集のない独立し、かつ
粒度分布がシャープなアルミナ粒子が特に高圧を必要と
することなく容易に得られる。特に燐酸塩を用いた場合
には板状アルミナ粒子が生成する。またハロゲン系の鉱
化剤を使用しないため、作業環境を汚染することがな
い。
According to the present invention, alumina particles free of aggregation and having a sharp particle size distribution can be easily obtained without particularly requiring a high pressure. In particular, when a phosphate is used, plate-like alumina particles are generated. Further, since no halogen-based mineralizer is used, the working environment is not polluted.

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 アルミン酸塩と酸性アルミニウム塩とを
水を含んだ状態で反応させることにより、アルミナ又は
/及びアルミナ水和物と中和金属塩を含む混合物を製造
し、この混合物を1000〜1600℃で焼成すること
を特徴とするアルミナ粒子の製造方法。
A mixture containing alumina and / or hydrated alumina and a neutralized metal salt is produced by reacting an aluminate and an acidic aluminum salt in a state containing water. A method for producing alumina particles, characterized by firing at 1600 ° C.
【請求項2】 アルミナ又は/及びアルミナ水和物が非
晶質又は/及び結晶質である請求項1記載のアルミナ粒
子の製造方法。
2. The method for producing alumina particles according to claim 1, wherein the alumina and / or alumina hydrate is amorphous or / and crystalline.
【請求項3】 アルミン酸塩と酸性アルミニウム塩と燐
酸塩とを水を含んだ状態で反応させる請求項1記載のア
ルミナ粒子の製造方法。
3. The method for producing alumina particles according to claim 1, wherein the aluminate, the acidic aluminum salt and the phosphate are reacted in a state containing water.
【請求項4】 アルミン酸塩にアルカリ性の燐酸塩を添
加したものと酸性アルミニウム塩を混合したものを水分
を含んだ状態で反応させる請求項1記載のアルミナ粒子
の製造方法。
4. The process for producing alumina particles according to claim 1, wherein a mixture of an aluminate and an alkaline aluminum phosphate and a mixture of an acidic aluminum salt are reacted in a state containing water.
【請求項5】 アルミン酸塩と酸性アルミニウム塩に酸
性の燐酸塩を添加したものを水分を含んだ状態で反応さ
せる請求項1記載のアルミナ粒子の製造方法。
5. The process for producing alumina particles according to claim 1, wherein an aluminate and an acidic aluminum salt to which an acidic phosphate is added are reacted in a state containing water.
【請求項6】 アルミン酸塩と酸性アルミニウム塩と燐
酸塩とを混合した時の水素イオン濃度がpH=6〜10
の範囲である請求項3〜5のいずれかに記載のアルミナ
粒子の製造方法。
6. A mixture of an aluminate, an acidic aluminum salt and a phosphate, having a hydrogen ion concentration of pH = 6-10.
The method for producing alumina particles according to any one of claims 3 to 5, wherein
【請求項7】 平均粒子径が0.2〜100μm、厚み
が3μm以下、アスペクト比(粒子径/厚み)が5以上
である板状アルミナ粒子を製造する請求項3〜6のいず
れかに記載のアルミナ粒子の製造方法。
7. A plate-like alumina particle having an average particle diameter of 0.2 to 100 μm, a thickness of 3 μm or less, and an aspect ratio (particle diameter / thickness) of 5 or more is produced. A method for producing alumina particles.
JP10007799A 1999-04-07 1999-04-07 Method for producing alumina particles Expired - Lifetime JP3711318B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10007799A JP3711318B2 (en) 1999-04-07 1999-04-07 Method for producing alumina particles

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10007799A JP3711318B2 (en) 1999-04-07 1999-04-07 Method for producing alumina particles

Publications (2)

Publication Number Publication Date
JP2000290013A true JP2000290013A (en) 2000-10-17
JP3711318B2 JP3711318B2 (en) 2005-11-02

Family

ID=14264394

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10007799A Expired - Lifetime JP3711318B2 (en) 1999-04-07 1999-04-07 Method for producing alumina particles

Country Status (1)

Country Link
JP (1) JP3711318B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002235026A (en) * 2001-02-09 2002-08-23 Sakura Color Prod Corp Solid drawing material
JP2003073603A (en) * 2001-08-30 2003-03-12 Sakura Color Prod Corp Ink composition for water ink ball-point pen, and ball- point pen using the same
JP2004155630A (en) * 2002-11-08 2004-06-03 Showa Denko Kk Alumina particle and method of manufacturing the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002235026A (en) * 2001-02-09 2002-08-23 Sakura Color Prod Corp Solid drawing material
JP4712200B2 (en) * 2001-02-09 2011-06-29 株式会社サクラクレパス Solid drawing material
JP2003073603A (en) * 2001-08-30 2003-03-12 Sakura Color Prod Corp Ink composition for water ink ball-point pen, and ball- point pen using the same
JP2004155630A (en) * 2002-11-08 2004-06-03 Showa Denko Kk Alumina particle and method of manufacturing the same

Also Published As

Publication number Publication date
JP3711318B2 (en) 2005-11-02

Similar Documents

Publication Publication Date Title
EP0722422B1 (en) Preparation of spheroidal aggregates of platy synthetic hydrotalcite
US6197277B1 (en) Process for producing alumina particles having high dispersibility and plasticity
JPS58176123A (en) Superpure boehmite and pseudoboehmite and manufacture thereof
WO2022110127A1 (en) Method for preparing cube-like nano calcium carbonate
JPH0574532B2 (en)
JPH0524844A (en) Production of hydrated zirconia sol and zirconia powder
CN112745105A (en) High-sintering-activity alumina ceramic powder and preparation method thereof
JP3759208B2 (en) Method for producing alumina particles
JP3711318B2 (en) Method for producing alumina particles
CN101646624A (en) Cubic magnesium oxide powder and method for producing the same
JP6068216B2 (en) Method for producing fluorapatite and method for producing fluorapatite fine particles
JP2006306677A (en) New zirconium phosphate
CN106995209B (en) A kind of ψ-type Zirconium phosphate crystal nanometer sheet and its preparation and application
JP2008137845A (en) Method of producing magnesium oxide
KR101440473B1 (en) Method for preparing plate-shaped alumina
JPS6242850B2 (en)
JP2000247634A (en) Production of alumina tabular grain
JPS6034496B2 (en) Manufacturing method of alumina sol
JPS6045125B2 (en) Manufacturing method of alumina sol
JPH01320220A (en) Magnesium hydroxide and its production
JP3237140B2 (en) Method for producing hydrated zirconia sol and zirconia powder
JPS62207705A (en) Crystalline aluminum phosphate and its preparation
KR100473399B1 (en) Process for the preparation of fine ceramic powders
JP3970208B2 (en) Method for synthesizing reactive oxygen species inclusion materials
JP3208768B2 (en) Method for producing hydrated zirconia sol

Legal Events

Date Code Title Description
A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A711

Effective date: 20040220

RD03 Notification of appointment of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7423

Effective date: 20040220

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20041129

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20050801

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20050815

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090819

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090819

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100819

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100819

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110819

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110819

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120819

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120819

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130819

Year of fee payment: 8

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

EXPY Cancellation because of completion of term